Article ID Journal Published Year Pages File Type
222291 Journal of Environmental Chemical Engineering 2015 8 Pages PDF
Abstract

The main disadvantage of immobilised catalytic systems is the loss of efficiency with respect to slurry systems. This is mostly due to the introduction of mass-transport limitations, and to the reduction of catalytic area. As a means of overcoming these issues, and building up on our previous studies, we investigated the merits of micro-structurisation of a tubular reactor by using glass micro-spheres as structurisation element and catalyst support. Two different reactor configurations were proposed and compared against dispersed slurry systems operating under similar conditions for the oxidation of a simulated wastewater containing phenol. The results show that catalyst immobilisation promoted an increase in the reaction rate constant, with respect to the slurry systems, of 29% when operating with an annular configuration, and 55% when employing a tubular configuration. The effect of a secondary feed of air or oxygen on the performance of immobilised systems was also investigated. The co-feeding of air promoted increases of 2.6 and 1.13 times in the reaction rate constant with respect to a single phase feed, for the annular and tubular configurations respectively; whereas the addition of pure oxygen enhanced the reaction rate to an even greater extent: 8.6 times for the annular and 4.3 times for the tubular configuration. These results reinforce our previous observations that micro-structured systems offer superior transport properties and increased contact between the catalyst and the reactants, thereby constituting an attractive alternative to suspended slurry photocatalysis.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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